US1045234A - Process of making artificial sponge. - Google Patents
Process of making artificial sponge. Download PDFInfo
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- US1045234A US1045234A US35561107A US1907355611A US1045234A US 1045234 A US1045234 A US 1045234A US 35561107 A US35561107 A US 35561107A US 1907355611 A US1907355611 A US 1907355611A US 1045234 A US1045234 A US 1045234A
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- curing
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- rubber
- sponge
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/36—Feeding the material to be shaped
- B29C44/46—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
- B29C44/50—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length using pressure difference, e.g. by extrusion or by spraying
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2075/00—Use of PU, i.e. polyureas or polyurethanes or derivatives thereof, as moulding material
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S264/00—Plastic and nonmetallic article shaping or treating: processes
- Y10S264/04—Molding and forming bendable and flexible product from rigid preform
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S264/00—Plastic and nonmetallic article shaping or treating: processes
- Y10S264/15—Aging of foamed resin products
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S264/00—Plastic and nonmetallic article shaping or treating: processes
- Y10S264/70—Processes for forming screens or perforating articles
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S521/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S521/918—Physical aftertreatment of a cellular product
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T152/00—Resilient tires and wheels
- Y10T152/10—Tires, resilient
- Y10T152/10279—Cushion
- Y10T152/10378—Casing enclosed core
- Y10T152/10387—Separate core
- Y10T152/10396—Removable
- Y10T152/10405—Sponge rubber
Definitions
- a further object of the invention is to provide an improved method of producing artificial sponge, having an intercellular body possessing in the maximum degree the power of absorbing and holding liquids.
- a quantity of the mixed compound is molded into the form approximating the desired shape of the completed article.
- These individual portions of the material may be molded in any convenient manner, as, for example, a convenient form may be employed in giving the mass the desired shape, as illustrated in Figure 1, in which the member or receptacle 1 shown in dotted lines indicates one-half of the mold, the top portion being removed while the remaining part 1 is used to hold the molded portions of the mixture when inserted into the curing oven.
- the part designated by the reference numeral 2 illustrates a crosssection of the material ready for insertion into the curing oven.
- the curing oven should be so constructed that live steam may be admitted to the interior thereof and in contact with the material to be cured.
- the curing is accomplishedvby closing and sealing the oven or curing receptacle and admitting steam until the material is suflicientlfy cured.
- Fig. 2 of the drawing is a view similar to 'Fig. 1 illustrating the material after ourcomes immediately from the curing oven. It will be observed that the action of the steam. and heat in curing the mixture has caused the gas producing material to gasify and so expand to a size many times its original proportions.
- Fig. 3 shows a cross-section of the cured portion as it appears aftercooling and contracting.
- the pressure of the gas punctures the wall of the cell, which. is produced by its formation during the a plication of heat in curing and the gas passes oil into the surrounding air in the oven after the manner of the escape of gases in the ordinary process of bakin bread.
- the gas is retained within the .cell and is kept from bursting through the walls in the surrounding material by reason of the steam pressure within the curing oven.
- the contact of the steam with the material alsoforms the exterior coating or covering 3 already described, which'assists in retaining the gas.
- next step in the process is to break down the v walls of the interior structure, thus relieving the vacuums created by the contraction ofthe gases and permitting the air to enter the interior of the structure, causing the material to assume its normal condltion, which is practically the condition it assumes in the illustration in Fig. 2, although somewhat smaller in size than the relative size exhibited in Fig. 2 for the reason that Fig.
- 60. 2 represents the material immediately after bein taken from the oven and under these conditions before contraction of the gases begins, the article is expanded to a greater extent than when under the pressure of the steam in the curing oven.
- Fig. 4 has been drawn to represent approximately the relative size of the completed article after the cell walls are broken down.
- the cell walls may be broken down by puncturing. them or forcing the gas from them in any conven i'ent manner, as, for example, by passing needles through the material; but the most approved method of accomplishing this result is illustrated in Figs. 5 and 6, which consists in passing the material between closely confined rollers.
- the apparatus for accomplishing this purpose preferably consists of two rollers, as 4 and 5, and may have their surface covered with some suitable ma-, 8o terial, such as hard rubber as used on ordinary clothes wringers. It is also desirable that these rollers be held together-by elastic pressure.
- Fig. 5 the material, as it appears in Fig. 3, is shown passing between the rollers in the direction indicated by the arrow. The material is repeatedly passed between the rollers in order to secure the complete breaking down of the cell walls.
- F ig, 6 i lus rates a view of the breaking down process similarto Fig. 5,-but showing material that has previously been passed between the rollers a number of times and discloses the fact that as .the proce% of breaking down the cell walls continues, the material continues to increase in its dimensions, particularly in thickness until finally the cell walls are all punctured or broken down and the air admitted to the interior throughout the entire structure, It will be apparent that-this breakin down of the interior structure or cell wa may readily be accomplished by a crushing or rocking process instead of the rollers, although, as stated, the use of the rollers is found to be the most satisfactory inpractice as regards economy of time and the production of an entirely satisfactory quality of the material.
- the breaking down of the cell walls by passing the material between the rollers it is foimd highly advantageous to vary the initial point ofcontact of the material with the rollers as'the frequent changes of direction in which the material is attacked or compressed by the rollers results in a more thorough breaking down of thecell walls and consequently abetter resulting quality of sponge material than if the material be presented to the rolls at each insertion in the same position.
- the final step in the production of the completed article consists in removing the exterior skin or covering 3.
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Description
G. H. WILLIS & B. P. FELIX. PROCESS or MAKING ARTIFICIAL SPONGE.
APPLIUATION FILED M1214 1967. v
' Patented Nov. 26, 1912.
UNITED STATES PAT GLENN H. WILLIS AND BENJAMIN F. FELIX, OF CHICAGO, ILLINOIS, ASSIG-NORS TO FEATHERWEIGHT RUBBER SPONGE COMPANY, OF G HICAGO, ILLINOIS, A GOR?ORA- TION OF ILLINOIS.
PROCESS OF MAKING ARTIFICIAL SPONGE.
Specification of Letters Patent.
Application filed February 4, 1907. Serial No. 355,611.
. clear, and exact specification.
degree the Theinvention-relates to artificial sponges and the primary object of the invention is to provide an improved method of producing an artificial sponge possessing to a superior qualities of porosity, elasticity, pliability, and capabilityfor the ready absorption of liquids.
A further object of the invention is to provide an improved method of producing artificial sponge, having an intercellular body possessing in the maximum degree the power of absorbing and holding liquids.
To the attainment of these ends and the accomplishment of other new and useful objects, aswill appear, the invention consists in the features of novelty in the processes hereinafter more fully described and claimed, and illustrated to an extent in the accompanying drawings, in which certain features of the preferred methods employed in" practising the invention are illustrated,
, as will appear by the references hereinafter known.
made to the various figures of the drawings. In the preferred manner of practising the invention, the raw rubber compound, as
commonly-sold on the market, is first thoroughly worked or mixed in a manner well During this working or mixing process, it is also common to introduce any desired coloring matter. Before this process of working or mixing of the compound is completed, the mixture should be thoroughly impregnated with any of the well known materials which are adapted to become' gaseous upon the application of heat, which is commonly applied in curing rubber. These materials are commonly applied to the mixture in liquid or granulated form, the granules of the material being very. finely pulverized when the material in form is used in order that the particles adapted to become gaseous may become very thoroughly mixed throughout the compound. The introduction of such materials into the compound and the mixing and coloring as described, are well known to those versed in the art, and has been commonly practised heretofore in the Patented Nov. 2c, 1912. V
production of various forms of dry cured sponge rubber, which is a common commercial article. Y
In practising the invention for-producing the toilet sponge, a quantity of the mixed compound is molded into the form approximating the desired shape of the completed article. These individual portions of the material may be molded in any convenient manner, as, for example, a convenient form may be employed in giving the mass the desired shape, as illustrated in Figure 1, in which the member or receptacle 1 shown in dotted lines indicates one-half of the mold, the top portion being removed while the remaining part 1 is used to hold the molded portions of the mixture when inserted into the curing oven. The part designated by the reference numeral 2 illustrates a crosssection of the material ready for insertion into the curing oven. It will be observed that an attempt has been made to illustrate the gas producing material with which the mixture is thoroughly impregnated, as described, by the strippling appearing throughout the section 2. The curing oven should be so constructed that live steam may be admitted to the interior thereof and in contact with the material to be cured. The curing is accomplishedvby closing and sealing the oven or curing receptacle and admitting steam until the material is suflicientlfy cured.
The time required for curing will, 0 course,
vary according to the amount of pressure applied. Heretofore, as already explained, it has been the practice to cure the material prepared as described, by what is known as the dry process; thatis, the steam is not -admitted into the interior of the oven or. curing receptacle, but the material iscured by .bemg placed on heated plates or in an oven heated from the exterior without the introduction of steam.
Fig. 2 of the drawing is a view similar to 'Fig. 1 illustrating the material after ourcomes immediately from the curing oven. It will be observed that the action of the steam. and heat in curing the mixture has caused the gas producing material to gasify and so expand to a size many times its original proportions.
ing and as it of forming a tough skin or covering around the exterior of the article as illustrated by the reference numeral 3 in Fig. 2. When the cured portions appearing as in Fig. 2 are removed from the oven, they cool very rapidly in coming into contact with the atmosphere, causing contraction of the gas within the cellular structure and consequent This is illustrated 0 collapse of the material.
in Fig. 3, which shows a cross-section of the cured portion as it appears aftercooling and contracting. In the common process of dry curing such material for the purpose of producing sponge rubber, the pressure of the gas punctures the wall of the cell, which. is produced by its formation during the a plication of heat in curing and the gas passes oil into the surrounding air in the oven after the manner of the escape of gases in the ordinary process of bakin bread. In the present improved process, owever, of curing the material under steam pressure, the gas is retained within the .cell and is kept from bursting through the walls in the surrounding material by reason of the steam pressure within the curing oven. The contact of the steam with the material alsoforms the exterior coating or covering 3 already described, which'assists in retaining the gas.
The illustration of the material after cool-- mg upon being taken out of the oven, as it appears in Fig. 3, only approximates thecondition of the material. The contraction of the cells gives the material a very shrunken and irregular appearance due to the partial vacuums formed in the multitude of cells by the contraction of the gases. The
next step in the process is to break down the v walls of the interior structure, thus relieving the vacuums created by the contraction ofthe gases and permitting the air to enter the interior of the structure, causing the material to assume its normal condltion, which is practically the condition it assumes in the illustration in Fig. 2, although somewhat smaller in size than the relative size exhibited in Fig. 2 for the reason that Fig.
60. 2 represents the material immediately after bein taken from the oven and under these conditions before contraction of the gases begins, the article is expanded to a greater extent than when under the pressure of the steam in the curing oven.
the gas within The illustration in Fig. 4 has been drawn to represent approximately the relative size of the completed article after the cell walls are broken down. The cell walls may be broken down by puncturing. them or forcing the gas from them in any conven i'ent manner, as, for example, by passing needles through the material; but the most approved method of accomplishing this result is illustrated in Figs. 5 and 6, which consists in passing the material between closely confined rollers. The apparatus for accomplishing this purpose preferably consists of two rollers, as 4 and 5, and may have their surface covered with some suitable ma-, 8o terial, such as hard rubber as used on ordinary clothes wringers. It is also desirable that these rollers be held together-by elastic pressure.
In Fig. 5 the material, as it appears in Fig. 3, is shown passing between the rollers in the direction indicated by the arrow. The material is repeatedly passed between the rollers in order to secure the complete breaking down of the cell walls. An attempt is made in Fig. 5 to illustrate the appearance of the material on itsfirst passage through the rollers. It will be observed that the. cell walls at the end of the material which was first to pass between the rollers do not show that they have been to any appreciable extent broken down, while the suc-' ceeding portions between the forward end and the position of the rollers inthis illustration appear to be more broken. This is the manner the rollers act on the material,
for the reason that when the material is first pinched or bit between the rollers many of the cells will at first be unbroken but as the material progresses between the rollers the 5 accumulations of the gas as'it' is crowded forward through the structure continues to increase and it will be'seen that the break-i ing of a single cell will force the gas there-- from into theadjoining cell, thus increasing that cell andfinally itself being forced into the-adjoining cell. This process of forcing the gas from one cell to another through the interior structure is continued until the gas is forced to the outer surface and breaks through the outer covering or skin 3, as indicated at 3, Fig.
5; When the material is first passed between the rollers, it willibe apparent that the process of. breaking the walls will ,dependupon the pressure applied to the gas contained within the sealed walls. However, as the breaking down process continues and the material begins to expand, the
air will enter from the exterior and being caught within the unbroken folds of the material by the action of the rollers, assists very materially in the further breaking,
" down of. the interior structure.
F ig, 6 i lus rates a view of the breaking down process similarto Fig. 5,-but showing material that has previously been passed between the rollers a number of times and discloses the fact that as .the proce% of breaking down the cell walls continues, the material continues to increase in its dimensions, particularly in thickness until finally the cell walls are all punctured or broken down and the air admitted to the interior throughout the entire structure, It will be apparent that-this breakin down of the interior structure or cell wa may readily be accomplished by a crushing or rocking process instead of the rollers, although, as stated, the use of the rollers is found to be the most satisfactory inpractice as regards economy of time and the production of an entirely satisfactory quality of the material. 1n the breaking down of the cell walls by passing the material between the rollers it is foimd highly advantageous to vary the initial point ofcontact of the material with the rollers as'the frequent changes of direction in which the material is attacked or compressed by the rollers results in a more thorough breaking down of thecell walls and consequently abetter resulting quality of sponge material than if the material be presented to the rolls at each insertion in the same position. The final step in the production of the completed article consists in removing the exterior skin or covering 3. This may be done by the use of a knife or other convenient means, but the most satlsfactory known method is to expose the surface of the sponge to a very sharp and rap-' idly-rotating cutter by which means the skin or covering'may be removed and the article shaped as desired Artificial sponge produced in the manner described possess to a superior degree thequality of ready absorption and subsequent retention of liquids for .the reason that the cell walls being broken down after curing have a valvular action due to the tendency of the adjacent slit or torn edges to co-' operate with each bther and close or partially close when the interior structure becomes filled with liquid.
In order that the invention might be fully understood, the details of the preferred manner of practising it have been thus specifically described, but
What we claim is:
1. The herein described process of making artificial sponge, which consists in curing a compound consisting of a thorough intermixture of rubber and a material adapted to assume gaseous form at temperatures 7 ordinarily employed in curing rubber.
whereby-contiguous closed cells are formed throughout the compound bv subjecting the compound to heat for curing and at the same time preventing uniformly throughout the resultingsubstance the breaking down of the contiguous cell walls during the curing operation by the application of external pressure, and after curing and cooling mechanically contiguous cells formed therein curing operation.
2-. .The herein described process of making artificial sponge, which consists in curing a compound of a thorough intermixture of rubber and a material adapted to assume gaseous form on the application of heat, whereby the resulting product becomes a cellular structure composed uniformly throughout of contiguous thinwalled closed cells, by subjecting the compound to the direct'action of steam under pressuresufiicient to counteract the tendency of the gases formed on the interior of the cells to break down the contiguous cell walls, and after cooling mechanically breaking down the walls of the contiguous cells formed during the curing operation to a deduring the gree whereby thorough intercommunication between contiguous cells is secured and the resulting material is rendered capable o the ready absorption of liquids.
3. The herein desecribed process of making artificial sponge which consists in curing a compound of rubber and a material adapted to assume gaseous form on the application of heat by subjecting the compound to the direct action of steam under pressure sufiicient to prevent the escape of the gases generated during the curing operation, whereby the resulting product becomes a cellular structure composed uniformly throughout of contiguous thinwalled closed cells, and after permitting the cooling and contraction of the resulting substance, mechanically breaking down the walls of the contiguous cells formed during the curing operation by thoroughlytearing or slitting them whereby complete in-" ter-communicatio'n between contiguous cells is secured and the resulting material is rendered capable of the ready absorption of liquids.
4. The herein described process of making artificial sponge which consists in curing a compound of rubber and a material adapted toassume gaseous form on the applicatlon of heat, by subjecting the compound to the direct'action of steam under pressure, and after permitting the cooling and contraction of the resulting substance, breaking down the walls of the cells formed during the operation of curing, by subjecting it to the crushing action of closely confined rolls.
5. The herein described process of making artificial sponge which consists in curing a compound of rubber and a material adaptedto assume gaseous form on the application of heat, by subjecting't-he compound to the direct action of steam under pressure; and
after permitting the. coohng and contraction of the resulting substance submitting it to a kneading or rolling process for the purpose of breaking down the cellular walls formed by the expansion of the gaseous material during the operation of curing.
. 6. The herein described process of making artificial sponge which consists in subjecting a cured compound of rubber and gaseous material having a plurality of closed gas retaining cells to a kneading or compressing pnfitess adapted to break down the said cell wa s.
7. The herein described process of making a material consisting of cured compound of rubber and gaseous material having a plurality of closed gas containing cells to the action of cooperating rollers, the said materialbeing repeatedly passed between the rollers, the initial point of contact of the material with the rollers being varied at each succeeding passage to break down the cell walls.
9. The herein described process of making artificial sponge which consists in subjecting a material consisting of cured compound of rubber and gaseous material having a plurality of closed gas containing cells to the action of cooperating rollers, the said material being repeatedly passed between the rollers, and shifted after each passage to vary the initial point of engagement of the material with the rollers to break down the cell walls.
10. The herein described process ofmaking artificial sponge which consists in cura compound of rubber and a material adapted to assume gaseous form at temperatures ordinarily employed in curing rubber, by subjecting the com ound under pressure to heat, and after curing breaking down the walls of cells formedduring the operation of curing by subjecting the cured material to a kneading or compressing process.
11. The hereindescribed process of making artificial sponge which consists in curing a compound of rubber and a material adapted to assume gaseous form at temperatures ordinarily employed in curing rubber, by subjecting the compound under pressure to heat, and after curing breaking down the walls of cells formed during the operation of curing by subjecting the cured material to the action of cooperating rollers.
12. The herein described process of making artificial sponge, which consists in ourmg a compound of rubber and a material adapted to assume gaseous form at temperatures ordinarily employed in curing rubher by subjecting the compound under conement or pressure to heat whereby the breaking down of the cell walls prematurely and during the curing operation -is prevented and after curing and cooling thoroughly tearing or slitting the cell walls by mechanical means whereby elongated openings 0r slits are formed in the cell walls uniformly throughout the resultlng structure, thus establishing thorough valvular intercommunication between adjacent cells. In testimony whereof we have signed our names to this specification, in the presence of two subscribing witnesses, on thls 31st day of January, A; D. 1907.
GLENN H. WILLIS. BENJAMIN F. FELIX. Witnesses:
HARRY Fromm, BENJAMIN B. Fnmx.
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Application Number | Priority Date | Filing Date | Title |
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US35561107A US1045234A (en) | 1907-02-04 | 1907-02-04 | Process of making artificial sponge. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US35561107A US1045234A (en) | 1907-02-04 | 1907-02-04 | Process of making artificial sponge. |
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US1045234A true US1045234A (en) | 1912-11-26 |
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US35561107A Expired - Lifetime US1045234A (en) | 1907-02-04 | 1907-02-04 | Process of making artificial sponge. |
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Cited By (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2434035A (en) * | 1938-04-15 | 1948-01-06 | Seamless Rubber Co | Process of making rubber gloves and like articles |
US2686747A (en) * | 1950-03-24 | 1954-08-17 | Nat Motor Bearing Co Inc | Method of manufacturing elastic sealing material |
US2758568A (en) * | 1953-09-11 | 1956-08-14 | Esterbrook Pen Co | Ink wells |
US2769205A (en) * | 1952-04-03 | 1956-11-06 | Rubatex Products Inc | Expanded cellular rubber with elliptical cells and method of making |
US2957832A (en) * | 1956-12-05 | 1960-10-25 | Gen Tire & Rubber Co | Cellular polyurethane elastomer and preparation of same using pyridine catalyst |
US2961710A (en) * | 1957-01-04 | 1960-11-29 | Norman H Stark | Method for making a foamed polyurethane filter |
US2993869A (en) * | 1956-12-05 | 1961-07-25 | Gen Tire & Rubber Co | Cellular polyurethane elastomer and preparation of same using a morpholine catalyst |
US3010148A (en) * | 1958-01-13 | 1961-11-28 | Crucible Steel Co America | Rolling mill |
US3046177A (en) * | 1958-03-31 | 1962-07-24 | C H Masland And Sons | Method of applying polyurethane foam to the backs of carpets and equipment therefor |
US3046172A (en) * | 1959-03-26 | 1962-07-24 | Standard Products Co | Spongy elastomeric materials and methods and products used in the manufacture of the same |
US3056753A (en) * | 1961-08-10 | 1962-10-02 | Koppers Co Inc | Treatment of expandable polymeric particles |
US3175025A (en) * | 1963-04-05 | 1965-03-23 | Chemotronics International Inc | Process for bonding and/or reticulation |
US3194854A (en) * | 1963-09-03 | 1965-07-13 | Dow Chemical Co | Process for producing thermoplastic foams |
US3240855A (en) * | 1962-11-16 | 1966-03-15 | Allied Chem | Fluffing foam |
US3281513A (en) * | 1962-12-07 | 1966-10-25 | Tecalemit Engineering | Method of manufacturing a fluid filter |
US3300558A (en) * | 1963-07-19 | 1967-01-24 | Walker Mfg Co | Method of removing the cell walls of a resilient cellular filter material |
US3342922A (en) * | 1963-10-09 | 1967-09-19 | Dow Chemical Co | Method of preparing re-expandable foam |
US3386877A (en) * | 1964-11-02 | 1968-06-04 | Dow Chemical Co | Cellular thermoplastic article having selected open cells and its manufacture |
US3394214A (en) * | 1964-08-10 | 1968-07-23 | Grace W R & Co | Method of increasing the tensile strength of a crosslinked ethylene polymer by compression |
US3403203A (en) * | 1964-03-13 | 1968-09-24 | Grace W R & Co | Method for preparing a non-woven fabric-like member |
US4274960A (en) * | 1977-11-09 | 1981-06-23 | Metzeler Ab | Filter means |
US4890485A (en) * | 1986-12-15 | 1990-01-02 | Hsu Charles J | Mechanism which reacts to the presence of oil and/or water |
-
1907
- 1907-02-04 US US35561107A patent/US1045234A/en not_active Expired - Lifetime
Cited By (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2434035A (en) * | 1938-04-15 | 1948-01-06 | Seamless Rubber Co | Process of making rubber gloves and like articles |
US2686747A (en) * | 1950-03-24 | 1954-08-17 | Nat Motor Bearing Co Inc | Method of manufacturing elastic sealing material |
US2769205A (en) * | 1952-04-03 | 1956-11-06 | Rubatex Products Inc | Expanded cellular rubber with elliptical cells and method of making |
US2758568A (en) * | 1953-09-11 | 1956-08-14 | Esterbrook Pen Co | Ink wells |
US2957832A (en) * | 1956-12-05 | 1960-10-25 | Gen Tire & Rubber Co | Cellular polyurethane elastomer and preparation of same using pyridine catalyst |
US2993869A (en) * | 1956-12-05 | 1961-07-25 | Gen Tire & Rubber Co | Cellular polyurethane elastomer and preparation of same using a morpholine catalyst |
US2961710A (en) * | 1957-01-04 | 1960-11-29 | Norman H Stark | Method for making a foamed polyurethane filter |
US3010148A (en) * | 1958-01-13 | 1961-11-28 | Crucible Steel Co America | Rolling mill |
US3046177A (en) * | 1958-03-31 | 1962-07-24 | C H Masland And Sons | Method of applying polyurethane foam to the backs of carpets and equipment therefor |
US3046172A (en) * | 1959-03-26 | 1962-07-24 | Standard Products Co | Spongy elastomeric materials and methods and products used in the manufacture of the same |
US3056753A (en) * | 1961-08-10 | 1962-10-02 | Koppers Co Inc | Treatment of expandable polymeric particles |
US3240855A (en) * | 1962-11-16 | 1966-03-15 | Allied Chem | Fluffing foam |
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